Olefinic impact modifiers for, and blends with, thermoplastic polyester resins

ABSTRACT

Thermoplastic polyester, copolyester and polyblend molding compositions impact-modified by glycidyl methacrylate grafted EPDM exhibit high impact strength combined with good knit-line characteristics, when the grafted comonomer content exceeds 2 percent by weight in the impact modifier, it has a gel content in the range of from about 10 to about 80 weight percent.

This is a divisional application of Ser. No. 07/235,432 filed on Aug.23, 1988, now U.S. Pat. No. 5,026,776 issued Jun. 25, 1991 which is acontinuation-in-part of Ser. No. 07/161,361 filed on Feb. 22, 1988, nowabandoned, which is a continuation-in-part of Ser. No. 07/004,089 filedJan. 16, 1987, now abandoned.

This invention relates to impact modified thermoplastic moldingcompositions and, more particularly, to glycidyl methacrylate orglycidyl acrylate grafted EPDM impact modifiers for thermoplasticpolyester, copolyester and polyblend molding compositions.

BACKGROUND OF THE INVENTION

High molecular weight linear polyesters and copolyesters of glycols andterephthalic or isophthalic acid have been available for a number ofyears. These are described inter alia in Whinfield et al., U.S. Pat. No.2,465,319, and in Pengilly, U.S. Pat. No. 3,047,539. These patentsdisclose that the polyesters are particularly advantageous as film andfiber formers.

With the development of molecular weight control, the use of nucleatingagents and two-step molding cycles, poly(ethylene terephthalate) or PEThas become an important constituent of injection moldable compositions.Further, poly(1,4-butylene terephthalate) or PBT, because of its veryrapid crystallization from the melt, is uniquely useful as a componentin such compositions. Work pieces molded from such polyester resins, incomparison with other thermoplastics, offer a high degree of surfacehardness and abrasion resistance, high gloss and lower surface friction.

Furthermore, in particular, poly(1,4-butylene terephthalate) is muchsimpler to use in injection molding techniques than poly(ethyleneterephthalate). For example, it is possible to injection moldpoly(1,4-butylene terephthalate) at low mold temperatures of from about30° to 60° C. to produce highly crystalline, dimensionally stablemoldings in short cycle times. Because of the high rate ofcrystallization, even at low temperatures, no difficulty is encounteredin removing the moldings from the molds. Additionally, the dimensionalstability of poly(1,4-butylene terephthalate) injection moldings is verygood even at temperatures near or well above the glass temperature ofpoly(1,4-butylene terephthalate).

However, the impact resistance of unmodified polyesters is relativelylow at room temperature and below. Thus for many applications, it isdesirable to have polyesters which are impact resistant at relativelyhigh and relatively low ambient temperatures. Yet, the other mechanicalproperties such as modulus of elasticity, tensile strength at yield andat break should be impaired either not at all or only to an acceptabledegree.

It has been recommended in various places to improve the impactresistance of polyesters by adding other polymers includinginterpolymers and copolymers. Specifically, the impact strength ofthermoplastic linear crystalline polyesters, including poly(1,4-butyleneterephthalate), has been improved by the incorporation therein of anethylene-propylene nonconjugated diene rubbery terpolymer (EPDM).Although EPDM is capable of impact-modifying BPT polyester compositions,e.g., Coran et al., U.S. Pat. No. 4,141,863 and Tanaka et al., U.S. Pat.No. 4,290,927, such compositions often suffer from "incompatibility"resulting in streaks or delamination of molded or extruded parts.

In Hepp, European Patent Application 0 149 192, abandoned published Jul.24, 1985, there is disclosed a thermoplastic molding compositionconsisting of a thermoplastic resin, e.g., polyester, copolyester orblock copolyester and an EPDM epoxidized with, e.g.,m-chloroperozy-benzoic acid. The examples given by this reference inTables 1, 2 and 3 do not, however, exhibit a combination of good impactstrength and acceptable knit-line characteristics.

Siegel, U.S. Pat. No. 3,769,260 discloses that a functionalized rubberimproves impact strength of polyesters, and suggests a range of 0.02 to20 microns in diameter for the dispersed rubber phase particles.

Epstein, U.S. Pat. No. 4,172,859, discloses the use of random copolymerscontaining various polar monomers. He also alludes to the use ofmaterials grafted with various polar monomers, e.g., glycidylmethacrylate (GMA), to impact modify thermoplastic polyesters includingPBT and PET. However, this patent does not deal with and therefore failsto recognize several factors that are critical to the function ofEPDM-G-GMA materials as impact modifiers for PBT systems. First, it doesnot recognize the benefits of reactive glycidyl (meth)acrylates as graftmonomers over non-reactive polar monomers such as maleic anhydride orn-vinyl pyrrolidone. Second, in Col. 5, lines 35-36, Epstein discountscrosslinking (gel formation) as unnecessary to the function of suchmodifiers, and states that crosslinking may be harmful. Third, theEpstein patent does not teach the need for a specific range of graftedGMA content in the rubber. Finally, Epstein discloses modifier particlesizes between 0.01-3.0 micron, and expressly states a distinctcriticality for particle size substantially entirely below 1 micron insize.

In Olivier, U.S. patent application Ser. No. 690,613, filed Jan. 11,1985, abandoned there are disclosed glycidyl methacrylate grafted EPDMimpact modifiers for polyester resins. In the specific examples, hedescribes materials having gel contents of less than 5 percent or morethan 48.7, with nothing in between. With little or no gel contents,i.e., 5 percent or less, he states that thermoplastic polyestercompositions with high impact strengths are obtained. With high gelcontents, specifically above 48.7%, Olivier discloses that the materialwas a much poorer impact modifier than one which was free of gel. In anyevent, the specific examples have subsequently been found not to providean acceptable combination of good impact strength and knit-linecharacteristics. Moreover, no mention is made of any effect of impactmodifier particle size on these important characteristics.

It has now been unexpectedly discovered that thermoplastic polyestercompositions comprising glycidyl methacrylate grafted EPDM (EPDM-g-GMA)impact modifiers can be prepared that possess high impact strengthcombined with good knit-line characteristics if careful attention ispaid to graft monomer content, gel content, and rubber particle size inthe impact modifier. The gel content preferably used is especiallyunexpected because it happens to fall in a range not actuallyinvestigated by Olivier. Compositions with these important propertieshave been developed as a result of numerous trials which haveestablished that it is required to use EPDM-G-GMA materials with greaterthan 2.0 percent, preferably greater than 3 percent, and especiallypreferably greater than 4 percent, GMA contents, and gel contents in the10-80 percent range. Impact properties are also vastly improved inthermoplastic blends with well-dispersed rubber particles in which morethan 60 percent, preferably more than 70 percent by weight of the rubberparticles are 1 micron or larger in diameter. Nothing in the prior artrenders such parameters obvious, and they cannot be developed by mereroutine optimization experiments.

SUMMARY OF THE INVENTION

In accordance with the present invention are provided impact modifiers,impact modified thermoplastic compositions, and methods for theirproduction, said modified thermoplastic compositions comprising:

(a) a high molecular weight thermoplastic polyester resin, and

(b) an effective amount of an impact modifier comprising an EPDMterpolymer grafted with 2% or more by weight, based on said terpolymerof glycidyl methacrylate or glycidyl acrylate or a mixture thereof,alone, or grafted in further combination with a C₁ -C₁₈ alkylmethacrylate or acrylate or a mixture thereof, component (b) having agel content in the range of 10 to 80 percent. Preferably, greater than60 percent by weight of the rubber particles therein are of 1 micron orlarger in diameter.

Also preferred herein is a composition as defined above wherein theEPDM-glycidyl ester grafted terpolymer is present in an amount of,approximately, 10 to 55 percent by weight based on the totalcomposition. Special mention is made of articles blow-molded from thecompositions of this invention.

DETAILED DESCRIPTION OF THE INVENTION

The high-molecular weight linear polyesters used in the practice of thepresent invention are polymeric glycol esters of terephthalic acid andisophthalic acid. They are available commercially or can be prepared byknown techniques, such as by the alcoholysis of esters of phthalic acidwith a glycol and subsequent polymerization, by heating glycols withfree acids or with halide derivatives thereof, and similar processes.These are described in U.S. Pat. No. 2,465,319 and U.S. Pat. No.3,047,539, and elsewhere.

Although the glycol portion of the polyester can contain from 2 to 10carbon atoms, it is preferred that it contain from 2 to 4 carbon atomsin the form of linear methylene chains.

Preferred polyesters will be of the family consisting of high molecularweight, polymeric glycol terephthalates or isophthalates having repeatedunits of the general formula: ##STR1## wherein n is a whole number offrom 2 to 4, and mixtures of such esters, including copolyesters ofterephthalic and isophthalic acids of up to about 30 mole percentisophthalic units.

Especially preferred polyesters are poly(ethylene terephthalate) andpoly(1,4-butylene terephthalate). Special mention is made of the latterbecause it crystallizes at such a good rate that it may be used forinjection molding without the need for nucleating agents or long cycles,as is sometimes necessary with poly(ethylene terephthalate).

Illustratively, high molecular weight polyesters will have an intrinsicviscosity-of at least about 0.7 deciliters/gram and, preferably, atleast 0.8 deciliters/gram as measured in a 60:40phenol-tetrachloroethane mixture at 30° C. At intrinsic viscosities ofat least about 1.0 deciliters/gram, there is a further enhancement oftoughness of the present compositions.

Capolyesters useful for the invention are preferably prepared fromterephthalic acid and/or isophthalic acid and/or a reactive derivativethereof and one or more glycols, which may be a straight or branchedchain aliphatic/cycloaliphatic glycol. Illustratively, the glycol willbe ethylene glycol; 2-methyl-1,3-propanediol, 1,4-butanediol;1,5-pentanediol; 1,6-hexanediol; 1,9-nonanediol; 1,10-decanediol;neopentylglycol; 1,4-cyclohexanediol; 1,4-cyclohexanedimethanol; amixture of any of the foregoing, or the like. Illustrative of suitablealiphatic dicarboxylic acids for the mixed aromatic/aliphaticembodiments are suberic, sebacic, azelaic, and adipic acids and thelike.

The copolyesters may be prepared by ester interchange in accordance withthe standard procedures. The copolyesters may preferably be derived fromat least 50% butylene terephthalate units.

The block copolyesters useful in the composition of this invention areprepared by the reaction of terminally reactive poly(1,4-butyleneterephthalate), preferably of low molecular weight, and a terminallyreactive copolyester or aliphatic polyester or both in the presence of acatalyst for transesterification, such as zinc acetate, manganeseacetate, titanium esters, and the like. The terminal groups can comprisehydroxyl, carboxyl, carboalkoxy, and the like, including reactivederivatives thereof. After initial mixing, polymerization is carried outunder standard conditions, e.g., 220° to 280° C., in a high vacuum,e.g., 0.1 to 2 mm Hg, to form the block copolymer of minimumrandomization in terms of distribution of chain segments. The result ofreaction between two terminally reactive groups, of course, must be anester linkage. These copolymers are described in a German Patentapplication P 27 56 167.7.

The copolyester designated component of these block copolyesters may beterminally reactive segments of copolyesters as described above. Thesecopolyesters are most preferably derived from an aliphatic glycol and amixture of aromatic and aliphatic diabasic acids in which the mole ratioconcentration of aromatic to aliphatic acids is from between 1 to 9 toabout 9 to 1, with an especially preferred range being from about 3 to 7to about 7 to 3.

The terminally reactive aliphatic polyester component of these blockcopolyesters will contain substantially stoichiometric amounts of thealiphatic diol and the aliphatic dicarboxylic acid, althoughhydroxy-containing terminal groups are preferred.

In addition to their ease of formation by well known procedures, boththe aforementioned aromatic/aliphatic copolyesters and aliphaticpolyesters are commercially available. One source for such materials isthe Ruco Division/Hooker Chemical Company, Hicksville, N.Y., whichdesignates its compounds as "Rucoflex".

The block copolyesters used in the invention preferably comprise fromabout 95 to about 50 parts by weight based on the block copolyesters ofpoly(1,4-butylene terephthalate) segments. The poly(1,4-butyleneterephthalate) blocks, before incorporation into the block copolyesters,will preferably have an intrinsic viscosity of about 0.1 dl./g. and,preferably, between about 0.1 and about 0.5 dl./g., as measured in a60:40 mixture of phenol-tetrachloroethane at 30° C. The balance 50 to 5parts by weight of the copolyester will comprise blocks of theaforementioned aromatic/aliphatic copolyesters and/or aliphaticpolyesters.

As will be understood by those skilled in the art, the poly(1,4-butyleneterephthalate) block can be straight chain or branched, e.g., by use ofa branching component, e.g., from about 0.05 to about 1 mole percent,based on terephthalate units of a branching component which contains atleast 3 ester-forming groups. This can be a polyol, e.g.,pentaerythritol, trimethylol-propane, and the like or a polybasic acidcompound, e.g., trimethyl trimestate, and the like.

Blends of the foregoing homopolymers, copolymers and/or block copolymersor derivatives thereof are also useful for the invention.

The glycidyl ester grafted terpolymer additives of this invention may beprepared from any of the well known EPDM terpolymer rubbers. EPDMterpolymers useful for preparing the grafted materials used in theinvention are commercially available, e.g., Copolymer Corp. (EPSYN® 55),or may be prepared using a Ziegler-type catalyst. The preparation oftypical EPDM terpolymers is described, for example, in Gresham et al.,U.S. Pat. No. 2,933,480; Tarney, U.S. Pat. No. 3,000,866; Guglielmino etal., U.S. Pat. No. 3,407,158; Gladding, U.S. Pat. No. 3,093,621 and U.S.Pat. No. 3,379,701. These terpolymers are characterized by the absenceof chain or backbone unsaturation and the presence of sites ofunsaturation in groups which are pendant to or are in cyclic structuresoutside of the main polymer chain.

Useful EPDM terpolymers for the production of the glycidyl ether graftedterpolymers used in this invention comprise ethylene, a C₃ to C₁₆straight or branched chain alpha-olefin, preferably propylene, and anon-conjugated diolefin, preferably propylene, and a non-conjugateddiolefin. Satisfactory non-conjugated dienes that may be used as thethird monomer in the terpolymer include straight chain dienes such as1,4-hexanediene, cyclic dienes such as cyclooctadiene and bridged cyclicdienes such as ethylidene norbornene.

Preferred EPDM terpolymers are comprised of about 10-95, preferably45-70 mole percent, by weight ethylene, about 5 to 90, preferably 30-55mole percent polypropylene and a minor amount of diene monomer, mostpreferably a polyunsaturated bridged ring hydrocarbon or halogenatedderivative thereof, most preferably 5-ethylidene-2-norbornene. TheseEPDM terpolymers have a melt index of approximately 79 g/10 min., aMooney viscosity of approximately 78 and a gram molecular weight ofabout 21,600.

The backbone rubber is subsequently graft modified with a graft monomerof epoxy functional acrylate or methacrylate. Although grafting mayoccur by various reaction mechanisms at practically any point on thebackbone rubber, generally, the grafting takes place at an unreactedpoint of unsaturation on the polyene. For this reason, it is desirableto make use of an ethylene, mono-olefin, polyene backbone rubber havingat least two unsaturated carbon-to-carbon linkages per 1000 carbon atomsand little additional benefit is derived from the use of unsaturatedbackbone rubber having more than 20 carbon-to-carbon double bonds per1000 carbon atoms. In the preferred practice of this invention, use ifmade of an unsaturated rubber having from 4-10 carbon-to-carbon doublebonds per 1000 carbon atoms.

The point of ethylenic unsaturation on the epoxy functional graftmonomer must be sufficiently reactive to react directly with theunsaturation of the polyene; or to react with a graft chain originatingat, or for combination with, the polyene unsaturation. Such levels ofreactivity require the alpha-beta situation of the ethylenicunsaturation as found in, for example, an epoxy functional esters ofacrylic acid or alkyl acrylic acid. A free radical initiator, such as adialkyl peroxide may be used to promote the graft reaction. In order toachieve the desired level of gel content, it is desirable to make use ofan initiator in an amount of at least 0.3 percent by weight of theunsaturated rubber. While more than 3 percent by weight initiator can beused to achieve the desired gel content, it is preferred to limit theupper range to about 3% by weight of the unsaturated rubber. It will benoted from the following examples that a higher amount of catalyst isdesired to achieve the level of gel content when the reaction is carriedout in solution (examples 1-3) for production of the impact modifier,while the desired level of gel content can be achieved at lower levelsof catalyst content when the reaction is carried out in bulk, asillustrated in examples 4-9. An amount of catalyst less than about 0.3percent by weight of the unsaturated rubber can be used, but the amountof working required for gel formation of the desired levels results inan undesirable amount of degradation of the backbone rubber.

Preferred as the graft monomer herein is glycidyl methacrylate (GMA).

The graft chain formed by the grafting process on the backbone rubberneed not be a homopolymer or even be of entirely epoxy functional graftmonomers. For example, combinations of the two above-mentioned epoxyfunctional graft monomers may be used as well as combinations of eitheror both with other C₁ -C₁₈ alkyl acrylates or methacrylates, wherein C₁-C₁₈ may be straight chain or branched, e.g., methyl, ethyl, isopropyl,2-ethyl-hexyl, decyl, n-octodecyl, and the like. Particularly usefulsuch comonomer grafts are grafts of glycidyl acrylate and/or glycidylmethacrylate and methyl methacrylate.

It is critical to the present invention that the gel content of theelastomeric material be controlled either during polymerization or insubsequent processing to achieve a value of greater than about 10% byweight and less than 80%. With a gel content too low impact strength ishigh, but knit-line strength is low. With a gel content too high, bothimpact strength and knit-line strength are low.

Gel content in an especially convenient analysis, according to ASTMD-3616, is measured by the weight percent of remaining elastomericmaterial after extraction in hexane or toluene. Gel content is anindication of the degree of cross-linking in the elastomeric material.Of course, persons skilled in the art are familiar with a variety ofways to control the degree of cross-linking and thus the gel content canbe determined by numerous other methods. The cross-link reaction may bea direct rubber backbone to rubber backbone joining, an epoxyfunctionality to epoxy functionality or rubber backbone joining, or agraft chain free radical addition to a second graft chain or to a rubberbackbone. Further, cross-linking may be achieved by the addition of across-linking agent to effectively achieve any of the above reactions.Thus, any of several steps to control gel content may be taken. Thermalaging will increase gel content. Increasing the amount of epoxyfunctional graft monomer will increase gel content. Increasing theamount of polyene monoene monomer in the rubber backbone will increasegel content. The addition of a cross-linking agent will increase gelcontent. The use of graft monomers with greater tendency to cross-linkwill increase gel content, for example, a homopolymer graft of glycidylacrylate will cross-link more readily than a homopolymer graft ofglycidyl methacrylate or a copolymer graft of glycidyl acrylate andmethyl methacrylate.

As stated above, gel content of the elastomeric material used in thisinvention should range up to no higher than about 80%. Althoughcross-linking can be carried on well past this level, as has beenmentioned, high levels of cross-linking diminish the dispersibility ofthe elastomeric material and lead to non-uniform mixing. Also, such highlevels of localized cross-linking will create brittle areas within theelastomeric material which will decrease rubbery character. It isapparent that cross-linking should be uniformly dispersed throughout theelastomeric material.

It is preferred in the present invention that the elastomeric materialhave an epoxy functionality of at least 2.5 epoxy functionalities per1000 carbon atoms, and preferably between about 5.0 and 13 epoxyfunctionalities per 1000 carbon atoms. Epoxy functionality means thoseepoxy sites which remain in the impact modifier resin after the loss ofsuch functionalities as may react in the cross-linking reaction. In theinstance of the use of GMA or GA as the epoxy functional graft monomer,a graft level of about 2% by weight is necessary to provide the minimumlevel of epoxy as shown above. The maximum is not particularly critical,e.g., up to 10-15% by weight can be used.

The grafting reaction may be carried out in solvent solution with theunsaturated rubber backbone present in a concentration which may rangefrom 10-30 percent by weight, with constant stirring, at an elevatedtemperature within the range of 125°-200° C. for a time ranging from 1/2to 2 hours. The reaction condition can be varied depending somewhat uponthe type and amount of catalyst and temperature conditions, as is wellknown to those skilled in the art. Where high amounts of graft monomerare to be attached to the backbone rubber, it has been found to beadvantageous to carry out the graft reaction in the melt state of thebackbone rubber, i.e., extruder grafting. This process is simplyperformed by feeding the backbone rubber, an excess of graft monomer,and an appropriate catalyst to a melt extruder and mixing and reactingthe feed components at an elevated temperature.

The above described elastomeric material is physically dispersed in athermoplastic polymer melt to form discrete particles of rubbery polymerin a continuous phase of a thermoplastic matrix resin or blend. At leastan impact strength improving amount of elastomeric material is dispersedin the matrix resin. Generally, this requires that the elastomericmaterial constitute at least 1.5 percent by weight, preferably 3.5 to 80percent, most preferably 10 to 55 percent, by weight based on totalthermoplastic content, including elastomeric material, of the moldingcomposition. It will be apparent that, while the indicated compositionrange is optimum for making toughened rigid plastic articles, acceptablemolding materials can still be made from mixtures with rubber contentsmuch higher than this range. Thermoplastic elastomer type moldingcompounds are produced when the elastomer content exceed 55 weightpercent, and even mixtures above the phase inversion composition, i.e.,those in which the thermoplastic resin phase is semi- or non-continouslyinterdispersed in a rubbery polymer matrix can be used to make flexiblemolded articles with excellent properties. 80 weight percent elastomeris a typical upper limit. Compounding of the rubber and thermoplasticresin is simply carried out by standard techniques, for example, bysimple melt blending or dry mixing and melt extruding at an appropriateelevated temperature for any given thermoplastic matrix. The resultantadmixture is then molded into a thermoplastic piece of specificdimensions or further extruded into a film or sheet product.

It is important to the final properties of molded parts containingelastomeric material that there is sufficient mixing in the extrusion ofthe resin melt. Herein, several reactions have been taught or suggestedto take place in the extruder and such are, of course, effected bymixing we well as residence time in the extruder. Thus, thorough mixingof the polymer melt is suggested and, depending upon the equipmentemployed, two successive extrusions of the melt may be required.

As has been mentioned, in preferred compositions the particle size ofthe rubber grafted with glycidyl esters will be selected to provide thatat least 60 weight percent of such particles, and preferably more than70 weight percent of them are greater than 1 micron in diameter. Suchcompositions combine optimum notched Izod impact strength, withknit-line strength, and these are vastly superior to those obtained withcompositions wherein, for example, only about 50 weight percent of theparticles exceed 1 micron in diameter. Particle size can be measured inany of the ways known in this art, but an especially convenient way isto use a computerized particle size analyzer to measure photomicrographsof scanning electron microscopy (SEM) images.

Compounding can be carried out in conventional equipment. For example,after pre-drying the thermoplastic polyester resin, e.g., at 125° C. for4 hours, a single screw extruder is fed with a dry blend of thepolyester and the additive ingredients, the screw employed having a longtransition and metering section to insure melting. On the other hand, atwin screw extrusion machine, e.g., a 28 mm Werner Pfleiderer machinecan be fed with resin and additives at the feed port. In either case, agenerally suitable machine temperature will be about 450° F. to 570° F.

The compounded composition can be extruded and cut up into moldingcomponents such as conventional granules, pellets, etc., by standardtechniques.

The compositions of this invention can be molded in any equipmentconventionally used for thermoplastic compositions. For example, withpoly(1,4-butylene terephthalate) good results will be obtained in aninjection molding machine, e.g., of the Newbury type with conventionalcylinder temperature, e.g., 450° F. and conventional mold temperatures,e.g., 150° F. On the other hand, with poly(ethylene terephthalate),because of the lack of uniformity of crystallization from interior toexterior of thick pieces, somewhat less conventional but still wellknown techniques can be used. For example, a nucleating agent such asLIOH, sodium stearate, graphite or a metal oxide, e.g., ZnO or MgO canbe included and standard mold temperatures of from about 150° F. to 230°F. will be used. Especially suitable in blow-molding.

It is to be understood that the foregoing compositions may contain otheradditives known in the art, including, but without limitation,nucleating agents, mold release agents, flow promoters, coloring agents,coupling agents, and stabilizers. The elastomeric containing moldingcompositions of this invention may be used as molding pellets and maycontain pigments, dyes, stabilizers, plasticizers, and the like. One mayreadily determine which are necessary and suitable for a particularapplication.

DESCRIPTION OF THE PREFERRED EMBODIMENTS

The following examples illustrate the invention. The claims are not tobe construed to be limited by them in any manner whatsoever.

In the examples the following designations are used to denote thematerials and physical tests employed:

    ______________________________________                                        Physical Tests                                                                RSV         Reduced solution viscosity measured in                                        a 0.1% solution of decalin at 135° C.                      Mooney Viscosity                                                                          ASTM D1646, ML + 4 (125° C.)                               Gel content ASTM D-3616                                                       Notched Izod                                                                              ASTM D256                                                         Impact                                                                        Unnotched Double                                                                          Variation of ASTM D256 where the test                             Gate Izod Impact                                                                          piece is double gate injection molded                                         from opposite ends under conditions                                           which center the tack line between the                                        ends of the test piece.                                           Ingredients                                                                   Backbone Rubber A                                                                         EPSYN ® resin; EPDM rubber; 2.2 RSV;                          (EPDM A)    9C = C/1000 C (8% by weight of polyene                                        5-ethylidene-2-norbornene); ethylene/                                         propylene ratio = 2/1; Mooney Viscosity =                                     40; Copolymer Rubber & Chemical Corp.                             Backbone Rubber B                                                                         EPSYN ® 55 resin; EPDM rubber; 2.3 RSV;                       (EPDM B)    9C = C/1000 C (8% by weight of polyene                                        5-ethylidene-2-norbornene); ethylene/                                         propylene ratio = 2/1; Mooney Viscosity =                                     50; Copolymer Rubber & Chemical Corp.                             Backbone Rubber C                                                                         EPSYN ® E901 resin; EPDM rubber; 2.2                          (EPDM C)    RSV; 4.5 C = C/1000 C (4% by weight of                                        polyene 5-ethylidene-2-norbornene);                                           E/P ratio 4/1; Mooney viscosity = 50;                                         Copolymer Rubber & Chemical Corp.                                 Antioxidant IRGANOX ® 1076 phenolic antioxidant;                                      Ciba Geigy Corporation                                            Initiator A Hercules Di-Cup.sup.R  free radical                                           initiator; dicumyl peroxide                                       Initiator B 2.5-dimethyl-2,5-di(t-butyl-peroxy)                                           hexane                                                            Poly(1,4-butylene                                                                         VALOX 315 resin; General Electric Co.                             terephthalate)/PBT                                                            ______________________________________                                    

Also in these examples, the following abbreviations are used:

PBT--poly(1,4-butylene terephthalate)

EPM--ethylene-propylene copolymer

EPDM--ethylene-propylene-polyene terpolymer

GMA--glycidyl methacrylate

GA--glycidyl acrylate

MMA--methyl methacrylate

EXAMPLES 1 AND 2

(a) Formulations of monomer grafted EPDM resin are prepared as follows:100 weight parts of backbone rubber A; 0.1 weight parts of antioxidant;and approximately 300 weight parts of hexane are charged to a one gallonHastelloy C reactor. The reactor is sealed, flushed with N₂, and heatedto 155° C. Specified weight parts of monomer (GMA or GA or GMA/MMA, asthe case may be) in approximately 15 weight parts hexane are meteredinto the reactor. This is followed by 2 weight parts of initiator A inapproximately 15 weight parts of hexane. The solution was stirred at500-600 rpm for one hour at 155° C. and 200-250 psig. After the reactionmixture has cooled down, the product is recovered by precipitation inacetone followed by drying overnight at 75° C. under pump vacuum.

(b) Thermoplastic compositions comprising poly(1,4-butyleneterephthalate) (PBT), and the rubber grafted material prepared in step(a) are extruded once on a single screw extruder. Zone temperatures are250° C., the die temperature is 240° C. and screw speed is 150 rpm. Thewater cooled strands of elastomeric material are cut into test piecesand notched Izod impact is measured according to ASTM D256. Thecompositions and results obtained are set forth in Table 1.

                  TABLE 1                                                         ______________________________________                                        Thermoplastic Compositions:                                                   Blends Extruded In A Single Screw Extruder                                                   Example                                                                       1A*   1B*    1C*     1   2                                     ______________________________________                                        Compositions (parts by weight)                                                PBT.sup.a        80      80     80    80  80                                  EPDM C.sup.b     20      --     --    --  --                                  EPM-g-N-vinylpyrrolidone.sup.c                                                                 --      20     --    --  --                                  EPM-g-maleic anhydride.sup.d                                                                   --      --     20    --  --                                  EPDM-g-GMA.sup.e --      --     --    20  --                                  EPDM-g-GA/MMA.sup.f                                                                            --      --     --    --  20                                  Properties                                                                    Notched Izod Impact (ft. lb./in)                                                               2.0     3.3    2.1   13.7                                                                              19.0                                ______________________________________                                         *Control                                                                      .sup.a VALOX ® 315, General Electric Company                              .sup.b EPSYN ® E901, Copolymer Rubber and Chemical Corporation.           .sup.c EPSYN ® 510, see footnote .sup.b for source, grafted with 5.8      wt. % Nvinyl pyrrolidone                                                      .sup.d EPSYN ® 7006, see footnote .sup.b for source, grafted with 0.6     wt. % maleic anhydride                                                        .sup.e Procedure of step (a), EPSYN ® 55 resin, grafted with 2.3 wt.      GMA                                                                           .sup.f Procedure of step (a), EPSYN ® 55, grafted with 2.0 wt. % GA  

The results indicate that vastly improved impact strength can beobtained by incorporating EPDM-g-GMA or EPDM-g-GA/GMA terpolymers intoPBT compositions, in comparison with EP rubbers grafted with other polarmonomers. Double extrusion of Example 1 raises the notched Izod value to18.7 ft.lbs./in. of notch.

EXAMPLES 3-7

(a) Rubber grafted materials are prepared following the procedure ofstep (a) in Examples 1 and 2 but using only glycidyl methacrylate as thegrafting monomer. The compositions made and their properties are setforth in Table 2.

                  TABLE 2                                                         ______________________________________                                        EPDM-grafted glycidyl methacrylate terpolymers                                           Procedure                                                                     3A    3B      3C      3D    3E                                     ______________________________________                                        Compositions                                                                  (parts by weight)                                                             EPDM A 4906  100     100     --    --    --                                   EPDM B 55    --      --      100   100   100                                  Hexane       300     300     400   400   400                                  GMA          2.5     10      1.5   1.5   1.5                                  Initiator A.sup.a                                                                          1.5     3       1.5   2.5   2.5                                  Properties                                                                    RSV          2.44    2.46    3.10  4.28  2.57                                 Bound GMA, % 2.60    2.76    1.51  1.88  2.26                                 Gel Content (wt. percent)                                                                  5       5       5     5     5                                    ______________________________________                                         .sup.a dicumyl peroxide, DiCup ®, Hercules Company                   

(b) 20 parts by weight of each elastomeric material of Procedures 3A-3Eare tumble blended with 80 parts by weight of poly(1,4-butyleneterephthalate) and 0.3 parts by weight of antioxidant and passed througha 3/4" Killion single screw extruder at extruder barrel and dietemperatures of 250° C. and screw speed of 100 rpm. The water cooledstrands are comminuted, dried, passed through the extruder a second timeunder identical conditions and pelletized. The pellets are dried andmolded into 1/8" test pieces on a 75 ton Newbury injection moldingmachine at a barrel temperature of 260° C. and a mold temperature of 65°C. Test results for blends containing the elastomeric materials areshown in Table 3.

                  TABLE 3                                                         ______________________________________                                        Thermoplastic Compositions PBT/EPDM-g-GMA terpolymers                                         Example                                                                       3    4      5      6    7                                     ______________________________________                                        Composition (parts by weight)                                                 PBT               80     80     80   80   80                                  Elastomeric Material (Bound                                                   GMA Content, %)                                                               Procedure 3A (2.6)                                                                              20     --     --   --   --                                  Procedure 3B (3.4)                                                                              --     20     --   --   --                                  Procedure 3C (1.51)                                                                             --     --     20   --   --                                  Procedure 3D (1.88)                                                                             --     --     --   20   --                                  Procedure 3E (2.26)                                                                             --     --     --   --   20                                  Properties                                                                    Notched Izod Impact                                                                             15.4   18.8   3.5  2.2  18.6                                (ft. lb./in.)                                                                 Unnotched Double Gate Izod                                                                      6.9    2.1    7.3  10.7 1.8                                 (ft. lb./in.)                                                                 ______________________________________                                    

The results listed in Table 3 show that high Izod impact values in theseblends are only achieved when the grafted EPDM rubbers have greater than2.0% bound GMA content.

PROCEDURE 4A

100 parts by weight of backbone rubber B; 0.1 parts by weight ofantioxidant; 8 parts by weight of glycidyl methacrylate; and 0.8 partsby weight initiator B are passed through a WP30 twin screw extruder.Zone temperatures are 200° C., the die temperature is 200° C., and screwspeed is 150 rpm. The water cooled strands of elastomeric material arechopped into pellets. Analysis of the pellets indicates 5.86 weightpercent glycidyl methacrylate and 17% by weight gel content.

PROCEDURE 4B

100 parts by weight of backbone rubber B; 0.1 parts by weight ofantioxidant; 7.4 parts by weight of glycidyl methacrylate; and 0.74parts by weight initiator B are passed through a WP57 twin screwextruder. Zone temperatures are 200° C., the die temperature is 200° C.,and screw speed is 160 rpm. The water cooled strands of elastomericmaterial are chopped into pellets. Analysis of the pellets indicates 5.4weight percent glycidyl methacrylate and 29% by weight gel content.

EXAMPLE 5

75 weight parts of the elastomeric material from Procedure 4A and 25weight parts of poly(1,4-butylene terephthalate) resin are passedthrough a Werner-Pfleiderer WP30 twin screw extruder at zonetemperatures of 230° C., a die temperature of 230° C. and a screw speedof 145 rpm. The resulting water cooled strands of elastomeric materialconcentrate are chopped into pellets. A composition according to thisinvention is obtained.

EXAMPLES 6 AND 7

33.1 parts by weight of poly(1,4-butylene terephthalate) resin; 100parts by weight of backbone rubber B; 0.1 parts by weight antioxidant;7.5 parts by weight glycidyl methacrylate; and 0.75 parts by weightinitiator B are tumble blended and passed through a 1" Killion extruderhaving an L/D ratio of 20/1. Zone temperatures are 220° C., the dietemperature is 205° C. and screw speed is 30 rpm. The air cooled strandsof elastomeric material are chopped into pellets. Bound glycidylmethacrylate and gel content were not directly measured. A compositionaccording to this invention is obtained.

A backbone rubber grafted under equivalent conditions, i.e., absentpoly(1,4-butylene terephthalate) resin and at lower zone temperatures of205° C. has a gel content of 15% and bound glycidyl methacrylate contentof 7 weight %. If this is melt blended with poly(1,4-butyleneterephthalate) a composition according to this invention will beobtained.

EXAMPLE 8

33.1 parts by weight of poly(1,4-butylene terephthalate) resin, 100parts by weight of a backbone rubber B, 0.1 parts by weight antioxidant,7.5 parts by weight of glycidyl methacrylate; and 0.75 parts by weightof initiator B, are passed through a WP30 twin screw extruder. Zonetemperatures are 230° C., the die temperature is 230° C., and screwspeed was 145 rpm. The initiator is dissolved in the glycidylmethacrylate and metered into the hopper through a gear pump. The watercooled strands of elastomeric material concentrate are chopped intopellets. Bound glycidyl methacrylate content is measured to be 6.1% byweight and equivalent gel content is estimated to be 15%. If 26.7 partsby weight of this composition is melt blended with 73.3 parts by weightof PBT, a composition in accordance with the present invention will beobtained.

EXAMPLES 9-11

(a) 100 parts by weight of backbone rubber B; 0.1 parts by weight ofantioxidant; 7.4 parts by weight of glycidyl methacrylate; and 0.56parts by weight of initiator B are passed through a WP57 twin screwextruder. Zone temperatures are 200° C.; and screw speed is 150 rpm. Thewater cooled strands of elastomeric material are chopped into pellets.Analysis of the pellets indicated 4.5 weight percent bound GMA and 21%gel.

(b) The elastomeric material of step (a) is tumble blended withpoly(1,4-butylene terephthalate) resin and antioxidant in varyingproportions as shown in Table 4. The blended mixtures are passed througha WP28 twin screw extruder at a zone temperature of 240° C., dietemperature of 240° C. and screw speed of 300 rpm. The water cooledstrands are pelletized. The pellets are dried and molded into 1/8" testpieces. Compositions and test results are shown in Table 4.

                  TABLE 4                                                         ______________________________________                                        Thermoplastic Compositions PBT/EPDM-g-GMA terpolymers                                            Example                                                                       9     10      11                                           ______________________________________                                        Compositions (parts by weight)                                                PBT                  90      85      80                                       Elastomeric material (step (a))                                                                    10      15      20                                       Antioxidant          0.3     0.3     0.3                                      Properties                                                                    Notched Izod Impact (ft. lb./in.)                                                                  2.4     12.4    15.5                                     Double Gate Unnotched Izod (ft. lb./                                                               20      20      20                                       in.)                                                                          Tensile Modulus (psi × 10.sup.3)                                                             283     253     216                                      ______________________________________                                    

The results of Table 4 indicate that the notched Izod strength of thesecompositions falls off dramatically below 15% elastomer content.

EXAMPLES 12-14

Blends of PBT/EPDM-g-GMA, 80:20 percent by weight, respectively, areprepared following the procedure of Examples 3-7. All blends wereextruded twice on a single screw machine. The compositions employed andthe results obtained are set forth in Table 5.

                  TABLE 5                                                         ______________________________________                                        Thermoplastic Compositions: PBT/EPDM-g-GMA Blends                                              Example                                                                       12      13     14                                            ______________________________________                                        Composition (parts by weight)                                                 Poly(1,4-butylene terephthalate).sup.a                                                           80        80     80                                        Rubber (EPDM)                                                                 EPDM-g-GMA.sup.b   20        20     --                                        EPDM-g-GMA.sup.c   --        --     20                                        Graft RSV.sup.d    2.43      gel*   gel*                                      Percent (%) GMA    2.36      5.86   4.18                                      Properties                                                                    Notched Izod Impact (ft. lb./in.)                                                                17.8      15.5   16.3                                      Unnotched Double Gate (ft. lb./in.)                                                              2.3       20     20                                        ______________________________________                                         .sup.a VALOX ® 315, General Electric Company                              .sup.b Backbone Rubber is EPDM B                                              .sup.c Backbone Rubber is EPDM C                                              .sup.d Rubber solution viscosity, dl/g.                                       *Rubber had a degree of crosslinking >15% which prevented solution            viscosity testing. All others had gel levels under 5%.                   

The results indicate that high notched Izod and double-gate impact (ameasure of knit-line strength) are obtained for impact-modified PBMcompositions where the rubber has combined high GMA contents with thepresence of a significant amount of gel (>15%).

EXAMPLES 15-17

The procedure of Examples 12-14 is followed except that in Examples 17the rubber is pelletized in an extruder before blending with PBT,extrusion and molding into compositions. Compositions and results areset forth in Table 6:

                  TABLE 6                                                         ______________________________________                                        Thermoplastic Compositions Effect of Pelletization                                             Example                                                                       15      16     17                                            ______________________________________                                        Compositions (parts by weight)                                                Poly(1,4-butylene terephthalate)                                                                 80        80     80                                        G162 (as prepared).sup.a                                                                         20        --     --                                        G196 (as prepared).sup.b                                                                         --        20     --                                        G196 (pelletized).sup.b                                                                          --        --     20                                        Percent GMA (%)    3.2       3.0    3.0                                       Percent (%) Gel    3         3      70                                        Properties                                                                    Notched Izod Impact                                                                              16.0      11.8   12.8                                      Unnotched DG Impact                                                                              2.2       1.9    15.8                                      ______________________________________                                         .sup.a EPSYN ® 55, 3.2% GMA, 3% gel as prepared                           .sup.b EPSYN ® 55, 3.0% GMA, 3% gel as prepared, 70% gel after            pelletizing by two passes through an extruder.                           

The results indicate that raising the gel content via pelletization isan effective way of improving knit-line strength.

EXAMPLES 18-20

The procedure of Examples 12-14 is followed except that the EPDM-g-GMArubber possesses a gel content of 29% and a grafted GMA content of 5.4%.As in Examples 12-14, these grafted EPDM's were used in 80:20 PBT/rubberblends except that the extrusion treatments were varied. Treatments andresults are set forth in Table 7.

                  TABLE 7                                                         ______________________________________                                        Thermoplastic Composition: Effect of Extrusion Treatment                                         Example                                                    Properties           18.sup.a                                                                              19.sup.b                                                                              20.sup.c                                 ______________________________________                                        Notched Izod Impact (ft. lb./in.)                                                                  14-16   15-16   13-14                                    Unnotched Double Gate Impact (ft. lb./                                                             2-3     20      20                                       in.)                                                                          ______________________________________                                         .sup.a 1× extrusion on WP 28 twin screw extruder                        .sup.b 1× extrusion on WP 28 twin screw extruder plus 1            

The results in Table 7 indicate that an increase in working, i.e.,extrusion steps improves the knit-line strength. Care must be taken,however, not to impart so much energy in working the polymer so that thecomposition is degraded due to heat and shear effects.

EXAMPLES 21-22

Molded articles prepared for testing from the compositions of Examples19 and 20 were examined under a scanning microscope (SEM). For this, theworkpieces were microtomed and etched in boiling toluene to remove theEPDM-g-GMA phases.

A computerized particle size analyzer was used to determine individualand average EPDM-G-GMA particle diameters from the SEM photomicrographs.Equivalent sphere volumes were then calculated from the diameters.Finally, the weight percent of EPDM-G-GMA (equivalent to volume percentin a single phase rubber) in particles larger than 1 micron (the upperlimit of Epstein, U.S. Pat. No. 4,172,859) was calculated. Results areset forth in Table 8:

                  TABLE 8                                                         ______________________________________                                        Thermoplastic Compositions:                                                   Computerized Particle Size Analysis                                                                Example                                                  Parameter              21       22                                            ______________________________________                                        Mean Particle Diameter, microns                                                                      0.590    0.461                                         Particle Diameter Range, microns                                                                     0.02-2.36                                                                              0.07-1.77                                     Weight Percent of Particles Larger than 1                                                            81.1     52.9                                          Micron in diameter                                                            ______________________________________                                    

The results in Table 8 indicate that the better notched Izod andknit-line strengths were found in the compositions that had over 80weight percent of the rubber in particles larger than 1 micron indiameter. The 2x extrusion treatment decreases the average particle sizesignificantly, and impact strength was slightly lower, but still over 50weight percent of the rubber was in particles larger than 1 micron.

EXAMPLE 23

The base rubber is the EPDM of Example 1. The rubber feed rate was 6.6pounds per hour to a Werner & Pfleiderer ZSK twin screw extruderoperating at a barrel temperature of 200° C. and a screw speed of 150rpm. Glycidyl methacrylate initiator and2,5-dimethyl-2,5-di(t-butylperoxy) hexane were fed continuously at ratesof 7.6 parts per hundred GMA and 0.40 parts per hundred initiator per100 parts by weight EPDM. The resulting reaction product had a gelcontent of 10%.

A most important concept of this invention resides in the inclusion of afraction of a polyester matrix resin as a fourth component forconcurrent reaction with the EPDM, methacrylate and/or acrylate andinitiator to produce what can be referred to as a "masterbatch" adaptedsubsequently to be blended with the remainder of the matrix resin asillustrated in Examples 6-9 of the application. In the absence of thesmall amount of the polyester (matrix) resin, the impact modifier tendsto agglomerate making it difficult in subsequent processing such ashandling, measuring and mixing the impact modifier with the matrix resinfor uniform dispersion therein. The inclusion of a fraction of thepolyester resin as a fourth component in the reaction results in apliable product that can be easily reduced to particulate form forhandling and distributing in subsequent processing steps.

In addition, it has been found that the presence of a small amount ofthe matrix resin as a component of the reaction, results in reactionwhich differs somewhat from the reaction that takes place in the absenceof the polyester and results in a masterbatch which appears to providefor a better blend with the matrix resin with which it is subsequentlycombined to provide an improved thermoplastic composition havingimproved properties.

The described improvements can be achieved when the reaction is carriedout in combination in which 10-80 percent by weight and preferably 20-50percent by weight of the total amount of polyester or other matrixresinous component of the final blend product. This intermediate, whichcontains a part of the matrix resin as a fourth component of thereaction, is referred herein as a masterbatch with which the remainderof the matrix resin is blended. Optimum results are secured when theunsaturated rubber component (EPDM) and matrix resin (polyester) arepresent in the masterbatch in the weight ratio of 50-80 parts by weightof the rubber polymer to 50-20 parts by weight of the matrix resin, andpreferably 60-80 parts by weight of the rubber polymer to 40-20 parts byweight matrix resin.

The above patents and publications are incorporated herein by reference.

Many variations will suggest themselves to those skilled in the art inlight of the above, detailed description. For example, instead of usingpoly(1,4-butylene terephthalate) as component (a), other polyesterresins, such as poly(ethylene terephthalate) or copolyesters derivedfrom one or more aliphatic and/or aromatic dicarboxylic acids and one ormore straight or branched chain aliphatic or cycloaliphatic glycolsincluding random or block copolyesters. Instead of injection molding,blow molding, including injection blow molding can be used. Instead of amixture of glycidyl methacrylate and methyl methacrylate a mixture ofgylcidyl acrylate and methyl methacrylate or a mixture of glycidylmethacrylate and octadecyl metacrylate can be used. Furthermore, otheradditives known to those skilled in the art may be added in conventionalamounts to the impact modified compositions herein including but withoutlimitation, nucelating agents, mold release agents, flow promoters,coloring agents, flame retardants, coupling agents and stabilizers.

All such obvious variations are within the full intended scope of theappended claims.

What is claimed is:
 1. The method of producing a masterbatch for meltblending with a polyester matrix resin to improve its knit-line strengthand toughness comprising reacting:(1) less than the full increment of ahigh molecular weight thermoplastic polyester matrix resin; (2) a rubberpolymer in the molten phase selected from the group consistingessentially of the interpolymerization reaction product of ethylene, oneor more C₃ -C₁₆ mono-olefins and a polyene; (3) a composition selectedfrom the group consisting of an epoxy functional acrylate, an epoxyfunctional methacrylate, an epoxy functional acrylate in combinationwith a C₁ -C₁₈ alkyl acrylate and an epoxy functional methacrylate incombination with a C₁ -C₁₈ alkyl acrylate; and (4) an initiator presentin an amount of at least 0.3 percent by weight of the rubber polymer toprovide a reaction product having a gel content in the range of fromabout 10 to about 80 percent.
 2. The method as claimed in claim 1 inwhich the rubbery polymer is formed by the interpolymerization ofethylene, propylene and 5-ethylidene-2-norbornene.
 3. The method asclaimed in claim 1 in which the ethylene and propylene are present inthe bound state in the ratio of 10-95 moles ethylene to 90-5 molespropylene.
 4. The method as claimed in claim 1 in which the polymer ispresent in an amount to provide up to 20 C═C groups per 1000 carbonatoms in the rubbery interpolymer.
 5. The method as claimed in claim 1in which the component (3) is glycidyl methacrylate.
 6. The method asclaimed in claim 1 in which the component (3) is glycidyl acrylate. 7.The method as claimed in claim 1 in which the component (3) is reactedin an amount of at least 2 percent by weight of the rubberyinterpolymer.
 8. The method as claimed in claim 1 in which the component(3) is reacted in an amount within the range of 2-15 parts per 100 partsby weight of the rubbery interpolymer.
 9. The method as claimed in claim1 in which the polyester resinous component (1) is present in an amountwithin the range of 10-80 percent by weight of the polyester resinpreent in the final product.
 10. The method as claimed in claim 1 inwhich the masterbatch is formulated to contain 20-50 percent by weightof the polyester resin in the final product.
 11. The method as claimedin claim 1 in which the ratio of rubbery interpolymer to polyester resinin the masterbatch is within the range of about 50-80 parts by weightrubbery interpolymer to 50-20 parts by weight of the polyester resin.12. The method as claimed in claim 1 in which the initiator is aperoxide catalyst present in an amount within the range of about 0.3 toabout 3.0 percent by weight of the rubbery interpolymer.
 13. Amasterbatch comprising the reaction product of:(1) less than the fullincrement of a high molecular weight thermoplastic polyester matrixresin; (2) a rubber polymer in the molten phase selected from the groupconsisting essentially of the interpolymerization reaction product ofethylene, one or more C₃ -C₁₆ mono-olefins and a polyene; (3) acomposition selected from the group consisting of an epoxy functionalacrylate, an epoxy functional methacrylate, an epoxy functional acrylatein combination with a C₁ -C₁₈ alkyl acrylate and an epoxy functionalmethacrylate in combination with a C₁ -C₁₈ alkyl acrylate; and (4) aninitiator present in an amount of at least 0.3 percent by weight of therubber polymer to provide a reaction product having a gel content in therange of from about 10 to about 80 percent.
 14. A masterbatch as claimedin claim 13 in which the ethylene and propylene are present in the boundstate in the ratio of 10-95 moles ethylene to 90-5 moles propylene. 15.A masterbatch as claimed in claim 13 in which the polymer is present inan amount to provide up to 20 C═C groups per 1000 carbon atoms in therubbery interpolymer.
 16. A masterbatch as claimed in claim 13 in whichthe component (3) is glycidyl methacrylate.
 17. A masterbatch as claimedin claim 13 in which the component (3) is glycidyl acrylate.
 18. Amasterbatch as claimed in claim 13 in which the component (3) is reactedin an amount of at least 2 percent by weight of the rubberyinterpolymer.
 19. A masterbatch as claimed in claim 13 in which thecomponent (3) is reacted in an amount within the range of 2-15 parts per100 parts by weight of the rubbery interpolymer.
 20. A masterbatch asclaimed in claim 13 in which the polyester resinous component (1) ispresent in an amount within the range of 10-80 percent by weight of thepolyester resin preent in the final product.
 21. A masterbatch asclaimed in claim 13 in which the masterbatch is formulated to contain20-50 percent by weight of the polyester resin in the final product. 22.A masterbatch as claimed in claim 13 in which the ratio of rubberyinterpolymer to polyester resin in the masterbatch is within the rangeof about 50-80 parts by weight rubbery interpolymer to 50-20 parts byweight of the polyester resin.
 23. A masterbatch as claimed in claim 13in which the initiator is a peroxide catalyst present in an amountwithin the range of about 0.3 to about 3.0 percent by weight of therubbery interpolymer.